US7001576B2 - Emulsifying and separating device for liquid phases - Google Patents

Emulsifying and separating device for liquid phases Download PDF

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Publication number
US7001576B2
US7001576B2 US10/296,063 US29606303A US7001576B2 US 7001576 B2 US7001576 B2 US 7001576B2 US 29606303 A US29606303 A US 29606303A US 7001576 B2 US7001576 B2 US 7001576B2
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US
United States
Prior art keywords
microchannels
cover plate
base plate
liquid phases
plate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related, expires
Application number
US10/296,063
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English (en)
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US20040026305A1 (en
Inventor
Michael Hohmann
Michael Schmelz
Günter Brenner
Hanns Wurziger
Norbert Schwesinger
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Merck Patent GmbH
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Merck Patent GmbH
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Publication date
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Assigned to MERCK PATENT GMBH reassignment MERCK PATENT GMBH ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: BRENNER, GUENTER, HOHMANN, MICHAEL, SCHMELZ, MICHAEL, SCHWESINGER, NORBERT, WURZIGER, HANNS
Publication of US20040026305A1 publication Critical patent/US20040026305A1/en
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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/432—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa
    • B01F25/4323—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa using elements provided with a plurality of channels or using a plurality of tubes which can either be placed between common spaces or collectors
    • B01F25/43231—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction with means for dividing the material flow into separate sub-flows and for repositioning and recombining these sub-flows; Cross-mixing, e.g. conducting the outer layer of the material nearer to the axis of the tube or vice-versa using elements provided with a plurality of channels or using a plurality of tubes which can either be placed between common spaces or collectors the channels or tubes crossing each other several times
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D11/00—Solvent extraction
    • B01D11/04—Solvent extraction of solutions which are liquid
    • B01D11/0496—Solvent extraction of solutions which are liquid by extraction in microfluidic devices
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/02—Separation of non-miscible liquids
    • B01D17/04—Breaking emulsions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/08—Thickening liquid suspensions by filtration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00—Other mixers; Mixing plants; Combinations of mixers
    • B01F33/30—Micromixers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00781—Aspects relating to microreactors
    • B01J2219/00783—Laminate assemblies, i.e. the reactor comprising a stack of plates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00781—Aspects relating to microreactors
    • B01J2219/00873—Heat exchange
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00781—Aspects relating to microreactors
    • B01J2219/00889—Mixing
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01L—CHEMICAL OR PHYSICAL LABORATORY APPARATUS FOR GENERAL USE
    • B01L3/00—Containers or dishes for laboratory use, e.g. laboratory glassware; Droppers
    • B01L3/50—Containers for the purpose of retaining a material to be analysed, e.g. test tubes
    • B01L3/502—Containers for the purpose of retaining a material to be analysed, e.g. test tubes with fluid transport, e.g. in multi-compartment structures
    • B01L3/5027—Containers for the purpose of retaining a material to be analysed, e.g. test tubes with fluid transport, e.g. in multi-compartment structures by integrated microfluidic structures, i.e. dimensions of channels and chambers are such that surface tension forces are important, e.g. lab-on-a-chip
    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N35/00—Automatic analysis not limited to methods or materials provided for in any single one of groups G01N1/00 - G01N33/00; Handling materials therefor
    • G01N2035/00465—Separating and mixing arrangements
    • G01N2035/00514—Stationary mixing elements

Definitions

  • the invention relates to a device for the emulsification and separation of small amounts of immiscible liquid phases.
  • the path to a miniaturised, continuous plant on a laboratory scale has hitherto primarily involved the development of individual microcomponents, such as pumps, mixers, reactors and heat exchangers; connection thereof in series enables chemical reactions to be carried out continuously in through-flow.
  • individual microcomponents such as pumps, mixers, reactors and heat exchangers
  • connection thereof in series enables chemical reactions to be carried out continuously in through-flow.
  • the larger the spatial distance between separately manufactured microcomponents of this type the more complex and difficult is precise control of the reaction parameters during the reaction, for example of the individual concentrations of substances participating in the reaction and the temperature or input of energy.
  • identical reaction conditions such as, for example, the temperature, can only be guaranteed at very great effort, if at all.
  • the object of the invention is therefore to provide an emulsification and separation device for two immiscible liquid phases in which the identical reaction conditions can be specified for the two process steps.
  • This object is achieved in accordance with the invention on the basis of a device which has a base plate and a cover plate which can be connected thereto, with microchannels cut out in the form of grooves on the inner surface of the base plate and/or cover plate, where two microchannels which can be filled separately through fill apertures in the base plate and/or cover plate cross one another a number of times in a mixing zone, the microchannels run together in a common microchannel in a subsequent separation zone, and, after a subsequent branch, are run to separate outlet apertures.
  • the emulsion formation which is highly dependent on the geometry, may be affected by the shaping of the microchannels, in particular the size of the mixing or separation zone.
  • the cross-sectional shape and surface structure of the cut-out microchannels can easily be matched to any desired application by means of precision-mechanical manufacturing methods.
  • the base plate and cover plate can optionally be made of metals, plastic or glass, each of which is suitable for certain chemical reactions, enabling use with an extremely wide variety of chemical substances.
  • the manufacturing complexity necessary for the production of the entire device is relatively low. Owing to the simple design, the device can be operated with virtually no maintenance, even in the long term. If a tight connection of the base plate to the cover plate is not effected through a material connection, but instead merely through pressure, the base plate and cover plate can easily be taken apart and cleaned in a simple manner.
  • either only the base plate or only the cover plate has microchannels cut out in the form of grooves. Instead, however, it is also possible to cut microchannels out on the corresponding surface of both the base plate and the cover plate.
  • the base plate and/or the cover plate has devices for temperature control.
  • An important property of microreaction systems is the large surface area of the microchannels relative to the liquid volume. Effective control and regulation of the heat balance is therefore possible, even in the case of highly endothermic or exothermic reactions. This is achieved in a simple manner by temperature control of the base plate and/or cover plate. Owing to the small cross sections of the microchannels and the resultant low volume flow rates, good heat exchange is ensured.
  • the base plate and the cover plate can be connected tightly by screws.
  • a connection which is usually sufficiently tight, even over long periods, is produced by screwing.
  • the base plate and cover plate can be separated from one another again, for example for simplified cleaning.
  • the outlet apertures of a device for the emulsification and separation of immiscible liquid phases can be connected to the inlet apertures of an adjacently arranged device. This facilitates multistep extraction by connecting a plurality of devices in series. Reaction mixtures can thus be worked up continuously, even on a small scale.
  • the single figure shows an exploded three-dimensional view of a device consisting of a base plate and a cover plate.
  • the illustrative example shown of the emulsification and separation device consists of a flat, rectangular base plate 1 and a cover plate 2 of similar shape.
  • Microchannels 4 , 4 a , 5 , 6 , 6 a cut out in the form of grooves are located on a surface 3 of the base plate 1 facing the cover plate 2 .
  • Two microchannels 4 , 4 a run on one side of the surface 3 in a wave shape crossing one another a number of times.
  • This zone referred to below for simplification as the mixing zone, terminates approximately in the centre of the surface 3 of the base plate 1 , where the two microchannels 4 , 4 a combine to form a common microchannel 5 .
  • the common microchannel 5 runs essentially straight.
  • separation zone separation of the immiscible liquid phases takes place on the basis of different physical properties, such as, for example, the surface tension.
  • the common microchannel 5 splits again into two outlet channels 6 , 6 a .
  • six screw holes 7 which are symmetrically distributed at the edges of the base plate 1 and of the cover plate 2 , are provided in each.
  • Two inlet apertures 8 , 8 a and two outlet apertures 9 , 9 a designed as cylindrical holes are located in the cover plate 2 , which covers the surface 3 of the base plate 1 . If the base plate 1 and the cover plate 2 are connected tightly, the two microchannels 4 , 4 a can be filled with liquid phases through the respectively assigned inlet apertures 8 , 8 a .
  • the liquid phases flow through the mixing zone, where effective emulsification of the two phases takes place. After separation of the two phases in the subsequent separation zone, the two phases exit again separately through the respective outlet apertures 9 , 9 a.
  • microchannels likewise designed in the same way as grooves to be cut out on the inner surface 3 a of the cover plate 2 .
  • the base plate 1 and the cover plate 2 may also be arranged differently, in particular the arrangement of the base plate 1 and of the cover plate 2 may be interchanged.
  • Another conceivable design variant is one in which one or more intermediate plates between the base plate 1 and the cover plate 2 can be tightly connected thereto and each have microchannels cut out on the inner surfaces.
  • FIG. 1 Illustrates an embodiment of the invention having a base plate ( 1 ) and cover plate ( 2 ).
  • FIG. 2 illustrates an embodiment of the invention where an intermediate plate ( 10 ) is present between the base plate ( 1 ) and cover plate ( 2 ).

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
US10/296,063 2000-05-23 2001-05-09 Emulsifying and separating device for liquid phases Expired - Fee Related US7001576B2 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE10025699A DE10025699A1 (de) 2000-05-23 2000-05-23 Emulgier- und Trennvorrichtung für flüssige Phasen
DE10025699.6 2000-05-23
PCT/EP2001/005283 WO2001089693A1 (de) 2000-05-23 2001-05-09 Emulgier- und trennvorrichtung für flüssige phasen

Publications (2)

Publication Number Publication Date
US20040026305A1 US20040026305A1 (en) 2004-02-12
US7001576B2 true US7001576B2 (en) 2006-02-21

Family

ID=7643383

Family Applications (1)

Application Number Title Priority Date Filing Date
US10/296,063 Expired - Fee Related US7001576B2 (en) 2000-05-23 2001-05-09 Emulsifying and separating device for liquid phases

Country Status (8)

Country Link
US (1) US7001576B2 (de)
EP (1) EP1284822A1 (de)
JP (1) JP2003534118A (de)
KR (1) KR100818564B1 (de)
AU (1) AU2001270515A1 (de)
DE (1) DE10025699A1 (de)
TW (1) TW574063B (de)
WO (1) WO2001089693A1 (de)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060113239A1 (en) * 2003-01-31 2006-06-01 Yoshihito Okubo Device and method of classifying emulsion and method of demulsifying emulsion
US7307104B2 (en) 2003-05-16 2007-12-11 Velocys, Inc. Process for forming an emulsion using microchannel process technology
US7485671B2 (en) 2003-05-16 2009-02-03 Velocys, Inc. Process for forming an emulsion using microchannel process technology
US7622509B2 (en) 2004-10-01 2009-11-24 Velocys, Inc. Multiphase mixing process using microchannel process technology

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB0208766D0 (en) * 2002-04-02 2002-05-29 Univ Surrey Liquid-liquid separation
EP1352688A1 (de) 2002-04-09 2003-10-15 Jean Brunner Miniaturisierter Probenhalter
US20040235299A1 (en) * 2003-05-22 2004-11-25 Axcelis Technologies, Inc. Plasma ashing apparatus and endpoint detection process
JP4348676B2 (ja) 2003-06-03 2009-10-21 富士フイルム株式会社 マイクロ化学装置
FR2871070B1 (fr) 2004-06-02 2007-02-16 Commissariat Energie Atomique Microdispositif et procede de separation d'emulsion
JP4640017B2 (ja) * 2005-07-29 2011-03-02 株式会社日立プラントテクノロジー 乳化装置
JP4852968B2 (ja) * 2005-10-24 2012-01-11 株式会社日立プラントテクノロジー 乳化方法とその装置
DE102008037901A1 (de) * 2008-08-15 2010-02-25 Bayer Technology Services Gmbh Vorrichtung und Verfahren zur Stofftrennung in einem mikrostrukturierten Apparat
DE102012103256A1 (de) 2012-04-16 2013-10-17 Karlsruher Institut für Technologie Mikrostrukturapparat mit optischer Oberflächengüte sowie Verfahren zur Herstellung desselben
CN111298481B (zh) * 2020-02-26 2022-02-01 东南大学 一种强湍流剪切微通道油水分离装置

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5595712A (en) 1994-07-25 1997-01-21 E. I. Du Pont De Nemours And Company Chemical mixing and reaction apparatus
WO1998010267A1 (en) 1996-09-04 1998-03-12 Technical University Of Denmark A micro flow system for particle separation and analysis
US5803600A (en) 1994-05-09 1998-09-08 Forschungszentrum Karlsruhe Gmbh Static micromixer with heat exchanger
WO1999064848A1 (en) 1998-06-08 1999-12-16 Caliper Technologies Corp. Microfluidic matrix localization apparatus and methods
EP0988886A2 (de) 1998-09-25 2000-03-29 MAN Nutzfahrzeuge Aktiengesellschaft Kompakter Kreuzkanalmischer

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999056862A1 (en) * 1998-05-07 1999-11-11 Purdue Research Foundation An in situ micromachined mixer for microfluidic analytical systems

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5803600A (en) 1994-05-09 1998-09-08 Forschungszentrum Karlsruhe Gmbh Static micromixer with heat exchanger
US5595712A (en) 1994-07-25 1997-01-21 E. I. Du Pont De Nemours And Company Chemical mixing and reaction apparatus
WO1998010267A1 (en) 1996-09-04 1998-03-12 Technical University Of Denmark A micro flow system for particle separation and analysis
WO1999064848A1 (en) 1998-06-08 1999-12-16 Caliper Technologies Corp. Microfluidic matrix localization apparatus and methods
US6306590B1 (en) * 1998-06-08 2001-10-23 Caliper Technologies Corp. Microfluidic matrix localization apparatus and methods
EP0988886A2 (de) 1998-09-25 2000-03-29 MAN Nutzfahrzeuge Aktiengesellschaft Kompakter Kreuzkanalmischer

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060113239A1 (en) * 2003-01-31 2006-06-01 Yoshihito Okubo Device and method of classifying emulsion and method of demulsifying emulsion
US7307104B2 (en) 2003-05-16 2007-12-11 Velocys, Inc. Process for forming an emulsion using microchannel process technology
US7485671B2 (en) 2003-05-16 2009-02-03 Velocys, Inc. Process for forming an emulsion using microchannel process technology
US7622509B2 (en) 2004-10-01 2009-11-24 Velocys, Inc. Multiphase mixing process using microchannel process technology
US7816411B2 (en) 2004-10-01 2010-10-19 Velocys, Inc. Multiphase mixing process using microchannel process technology

Also Published As

Publication number Publication date
EP1284822A1 (de) 2003-02-26
AU2001270515A1 (en) 2001-12-03
KR100818564B1 (ko) 2008-04-01
TW574063B (en) 2004-02-01
US20040026305A1 (en) 2004-02-12
JP2003534118A (ja) 2003-11-18
WO2001089693A1 (de) 2001-11-29
KR20030019393A (ko) 2003-03-06
DE10025699A1 (de) 2001-12-06

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